








key: cord-011320-cwvkox29
authors: Puente-Massaguer, Eduard; Lecina, Martí; Gòdia, Francesc
title: Integrating nanoparticle quantification and statistical design of experiments for efficient HIV-1 virus-like particle production in High Five cells
date: 2020-01-06
journal: Appl Microbiol Biotechnol
DOI: 10.1007/s00253-019-10319-x
sha: 
doc_id: 11320
cord_uid: cwvkox29

The nature of enveloped virus-like particles (VLPs) has triggered high interest in their application to different research fields, including vaccine development. The baculovirus expression vector system (BEVS) has been used as an efficient platform for obtaining large amounts of these complex nanoparticles. To date, most of the studies dealing with VLP production by recombinant baculovirus infection utilize indirect detection or quantification techniques that hinder the appropriate characterization of the process and product. Here, we propose the application of cutting-edge quantification methodologies in combination with advanced statistical designs to exploit the full potential of the High Five/BEVS as a platform to produce HIV-1 Gag VLPs. The synergies between CCI, MOI, and TOH were studied using a response surface methodology approach on four different response functions: baculovirus infection, VLP production, VLP assembly, and VLP productivity. TOH and MOI proved to be the major influencing factors in contrast with previous reported data. Interestingly, a remarkable competition between Gag VLP production and non-assembled Gag was detected. Also, the use of nanoparticle tracking analysis and flow virometry revealed the existence of remarkable quantities of extracellular vesicles. The different responses of the study were combined to determine two global optimum conditions, one aiming to maximize the VLP titer (quantity) and the second aiming to find a compromise between VLP yield and the ratio of assembled VLPs (quality). This study provides a valuable approach to optimize VLP production and demonstrates that the High Five/BEVS can support mass production of Gag VLPs and potentially other complex nanoparticles. ELECTRONIC SUPPLEMENTARY MATERIAL: The online version of this article (10.1007/s00253-019-10319-x) contains supplementary material, which is available to authorized users.

Virus-like particles (VLPs) have emerged as promising nanoparticles, particularly in the field of new recombinant vaccines (Mohsen et al. 2017) . Compared with other conventional vaccines such as live-attenuated or inactivated viruses, VLPs can elicit potent antibody and T cell responses in a safe manner since they do not contain genetic material from the virus itself (Andersson et al. 2018 ). Among the different proteins able to self-assemble as VLPs, the group-specific antigen (Gag) polyprotein has demonstrated a wide applicability in different research areas. These include their use as immunogens (Young and Ross 2006) , drug delivery vehicles (Deo et al. 2015) , scaffolds for surface antigen presentation (Vidigal et al. 2018) , and research surrogates . A common need in all these applications is the understanding of the production system itself, which is paramount to define the most adequate conditions for VLP production.

The baculovirus species Autographa californica multiple nucleopolyhedrovirus (AcMNPV) has been successfully used for the production of a variety of VLP types. The ease of handling, the high productivities associated and the capacity to accommodate large quantities of DNA have made the baculovirus expression vector system (BEVS) a very attractive platform (Fernandes et al. 2013; Gómez-Sebastián et al. 2014) . From the different available insect cell lines, High Five Electronic supplementary material The online version of this article (https://doi.org/10.1007/s00253-019-10319-x) contains supplementary material, which is available to authorized users. cells have been reported to produce high VLP titers with a reduced level of contaminant baculovirus (Senger et al. 2009 ). In fact, Cervarix®, the first VLP-based human papillomavirus vaccine approved, is produced using the High Five/BEVS. Recent advances in the field of nanoparticle quantification and characterization have brought the opportunity to deepen into the understanding of the BEVS. In the frame of initiatives such as Process Analytical Technologies (PAT), the application of new and more sophisticated characterization technologies will be a powerful tool to increase the understanding of how the process conditions influence the quality of the final product. Nanoparticle tracking analysis (NTA) and flow virometry are gaining interest as tools to monitor the production of different particles, including VLPs (Nika et al. 2019; Pereira Aguilar et al. 2019) . To date, most of the studies dealing with VLP production are performed with indirect quantification methods based on monomer detection, which hinder the appropriate assessment of the final product and the yields obtained (Haynes et al. 2009; Pillay et al. 2009; Visciano et al. 2011 ). In addition, the simultaneous production of extracellular vesicles (EV), which frequently fall in the size range of VLPs, is not often considered and may lead to an erroneous estimation of VLP titers. With the aim to deepen in the characterization of the different existing nanoparticle populations, the eGFP was fused in frame to the gag gene from the human immunodeficiency virus serotype 1 (HIV-1).

Considering the information from previous reports, we decided to apply these novel techniques for optimizing the Gag VLP production process using the High Five/BEVS platform. Different methods are available for process improvement, from the classical one-variable-at-a-time approach to more sophisticated statistical design of experiments (DoE) (Puente-Massaguer et al. 2019) . So far, VLP production studies have focused either on the former approach (Krammer et al. 2010; Pushko et al. 2017) or on simple factorial designs (Pillay et al. 2009; Pastor et al. 2019) , limiting the analysis of higher order effects between the variables influencing VLP production. This is of special relevance since the use of lower or higher MOI than strictly required might reduce the maximum VLP yield obtained or be detrimental to the system, respectively. Here, we applied a response surface methodology (RSM) to evaluate the impact of cell concentration at infection (CCI), multiplicity of infection (MOI), and time of harvest (TOH) on VLP production. To go a step further in process understanding, the inclusion of several responses during process optimization has shown successful results and applicability in different research areas (Pinzi et al. 2011; Honary et al. 2014; Bukzem et al. 2016) . Particularly, the three responses considered in addition to VLP production were VLP assembly, baculovirus infection, and VLP productivity. These are of special relevance in processes with recombinant baculovirus since it is desirable to define production conditions encompassing high production yields with an acceptable ratio of correctly assembled Gag in the form of VLPs, but at the same time maintaining high productivities. A multiple-criteria decision analysis (MCDA) was implemented to combine the RSM-optimized responses into a global optimal set of conditions based on two criteria: quantity and quality. The two optimal production conditions were successfully validated, and the quantity optimum was compared with other Gag VLP production strategies using the High Five/BEVS. Finally, the correct formation and morphology of the VLPs produced was characterized using cryogenic transmission electron microscopy (cryo-TEM). The results presented in this work represent an advance with respect to current literature related to Gag VLP production in the High Five/BEVS and provide useful insights into nanoparticle-based process characterization.

High Five (cat. num. B85502, Thermo Fisher Scientific, Grand Island, NY, USA) and Sf9 cells (cat. num. 71104, Merck, Darmstadt, Germany) were cultured in suspension in the lowhydrolysate content and animal origin-free Sf900III medium (Thermo Fisher Scientific). Both cell lines were routinely maintained at exponential growth phase in 125-mL disposable polycarbonate Erlenmeyer flasks (Corning, Steuben, NY, USA) in 15 mL of medium and subcultured three times a week at a density of 2-4 × 10 5 cells/mL for High Five cells (Puente-Massaguer et al. 2018 ) and 4-6 × 10 5 cells/mL for Sf9 cells (Puente-Massaguer et al. 2020) . All cultures were shaken at 130 rpm using an orbital shaker (Stuart, Stone, UK) and maintained at 27°C in an incubator. Cell count and viability were performed using the Nucleocounter NC-3000 (Chemometec, Allerod, Denmark) according to manufacturer's instructions.

The recombinant Autographa californica multicapsid nucleopolyhedrovirus (AcMNPV), containing the HIV-1 Gag matrix protein fused in frame to eGFP (BV-GageGFP) (Hermida-Matsumoto and Resh 2000) and under the control of the polyhedrin promoter, was constructed using the BaculoGold system (BD Biosciences, San Jose, CA, USA). Baculovirus amplification was performed in the Sf9 cell line (cat. num. 71104, Merck, Darmstadt, Germany) cultured in Sf900III medium by infection at 3 × 10 6 cells/mL, a multiplicity of infection (MOI) of 0.1, and harvest at 96 hours post infection (hpi).

Titration of baculovirus infectious particles was conducted using the plaque assay method. Briefly, 2 mL of Sf9 cells at a concentration of 0.5 × 10 6 cell/mL was plated per well in 6well plates (Nunc, Roskilde, Denmark) and left to attach for 30 min at RT. Then, the Sf900III medium was aspired and Sf9 cells were infected with the addition of 1 mL per well of serial dilutions (10 −4 to 10 −9 ) of the BV-GageGFP samples. Six well plates were incubated at very mild mixing conditions during 1 h to homogeneously distribute the baculoviruses. Afterwards, baculovirus-containing supernatants were aspired and 2 mL of a type VII-A agarose (Merck) solution warmed at 42°C was added per well to cover the infected cells. The agarose solution was prepared by mixing an ultrapure water solution containing 3% w/v agarose with Sf900III medium supplemented with 10% fetal bovine serum (FBS) at a 1:1 ratio. After agarose cooling, 2 mL of Sf900III medium supplemented with 10% FBS was added per well and the plates were incubated for 5 days at 27°C without agitation. The concentration of infectious baculovirus particles, expressed as plaque forming units (pfu), was measured by visual inspection after 3 h staining with a 0.3% w/v Neutral Red solution (Merck) prepared in DPBS.

Cell growth and infection studies were performed in High Five cell cultures seeded at 3 × 10 5 cell/mL in 15 mL and maintained at mid-exponential phase by cell passaging every 48 h. Several MOI, cell concentrations at infection (CCI), and times of harvest (TOH) were evaluated and the different parameter combinations were defined according to a DoE-based approach. Samples were taken every 12-24 h to monitor viable cell concentration, cell viability, baculovirus infection, intra-and extracellular GageGFP expression, and nanoparticle production. Samples were harvested by centrifugation at 3000×g for 5 min and supernatants were maintained at 4°C until analysis. Cell pellets were stored at − 20°C.

The percentage of GageGFP expressing cells was assessed using a BD FACS Canto II flow cytometer equipped with a 488-nm laser configuration (BD Biosciences). Briefly, 0.3 mL of infected cell cultures was harvested by centrifugation at 300×g for 5 min and fixed using 4% p-formaldehyde for 10 min. Cells were then centrifuged at 500×g for 5 min to remove p-formaldehyde, resuspended in 0.3-mL ice-cold DPBS (Thermo Fisher Scientific), and maintained at 4°C until further analysis.

BV-GageGFP-infected High Five cells were observed using a TCS SP5 confocal microscope (Leica, Wetzlar, Germany). Cells were stained with 0.05% v/v of CellMask™ and 0.1% v/v of Hoechst (Thermo Fisher Scientific) to visualize the lipid membrane and cell nucleus, respectively. A washing step prior to observation was performed by centrifugation at 300×g during 5 min, and then cells were resuspended in fresh Sf900III medium. Samples were placed in 35-mm glass bottom Petri dishes with a 14-mm microwell (MatTek Corporation, Ashland, MA, USA) for visualization. The VLP production process was monitored during 6.5 min at 48 hpi using the Resonant scanner mode of the confocal microscope (Leica).

The amount of GageGFP produced by High Five infected cells was measured intra-and extracellularly by spectrofluorometry. Supernatants of GageGFP producing cells were harvested by centrifugation at 3000×g for 5 min and maintained at 4°C until analysis. Intracellular GageGFP content was evaluated by disruption of pelleted cells by means of three freeze-thaw cycles (2.5 h frozen at − 20°C and thawed at 37°C for 0.5 h). Samples were vortexed for 5 s between cycles. Lysed pellets were resuspended in 0.5 mL of TMS buffer (50-mM Tris-HCl, 150-mM NaCl, 2-mM MgCl 2 , pH 8.0), centrifuged at 13,700×g for 20 min and kept at 4°C. GageGFP fluorescence was measured with a Cary Eclipse fluorescence spectrophotometer (Agilent Technologies, Santa Clara, CA, USA) at RT as follows: λ ex = 488 nm (5-nm slit), λ em = 500-530 nm (10-nm slit). 

The Sf900III medium and a 0.1 mg/mL quinine sulfate solution were used as control patterns to normalize RFU values in samples between different experiments.

A NanoSight NS300 (Malvern Panalytical, Malvern, UK) was used to measure fluorescent and non-fluorescent particles by nanoparticle tracking analysis (NTA). Samples were diluted in 0.22-μm-filtered DPBS and continuously injected into the device chamber through a pump at an average concentration of 10 8 particles/mL (20-60 particles/frame). Videos of 60 s from independent triplicate measurements were analyzed with the NTA 3.2 software at RT. The nanoparticle number was evaluated in the 100-250-nm range.

Fluorescent and non-fluorescent nanoparticles were also analyzed using a CytoFlex LX (Beckman Coulter, Brea, CA, USA) equipped with a 488-nm blue laser for fluorescent particle detection and a 405 nm laser/violet side scatter configuration for improved nanoparticle resolution. Samples were diluted in 0.22-μmfiltered DPBS and triplicate measurements from independent samples were analyzed with the CytExpert 2.3 software at RT.

Supernatants of BV-GageGFP-infected High Five cells harvested at the different conditions of the DoE were ultracentrifuged in a double cushion of 5 mL of 25% and 8 mL of 45% (w/v) sucrose (Merck) solution prepared in DPBS and DMEM (Thermo Fisher Scientific), respectively. Five milliliters of supernatants from triplicate experiments were loaded in ultracentrifuge tubes (Beckman Coulter) and filled to the top with sterile DPBS. Sample ultracentrifugation was performed in a Beckman Optima L100XP centrifuge (Beckman Coulter) equipped with a SW-32Ti rotor at 31,000 rpm for 2.5 h at 4°C. Samples were taken from each ultracentrifuge fraction, and pellets were resuspended in 100 μL of DPBS and kept overnight at 4°C. All samples were stored at − 20°C until their measurement by spectrofluorometry and at 4°C for nanoparticle analysis by flow virometry. The same procedure was applied to characterize the optimal conditions obtained with the DoE and the MCDA approach.

Cryogenic transmission electron microscopy VLP morphology was assessed using a transmission electron microscope equipped for sample cryogenics (cryo-TEM). Briefly, 4 μL of sample was blotted onto EMR Holey carbon films on 400-mesh copper grids (Micro to Nano, Wateringweg, Netherlands) previously subjected to a glow discharge treatment in a PELCO easiGlow™ Discharge Cleaning System (PELCO, Fresno, CA, USA). Deposited samples were then plunged into liquid ethane at − 180°C using a Leica EM GP workstation (Leica) and observed in a JEM-2011 TEM operating at 200 kV (Jeol Ltd., Akishima, Tokyo, Japan).

A response surface methodology (RSM) was applied to assess the effect of the main factors influencing the BEVS: CCI (cell/mL), MOI (pfu/cell), and TOH (h) on different responses. The selected DoE responses were baculovirus infection (% of infected cells), VLP production (fluorescent particle/mL), GageGFP polyprotein assembled in the form of VLPs (% of GageGFP assembled as VLPs), and VLP productivity (fluorescent particle/mL h). VLP production and VLP productivity responses were transformed to log values using the logarithmic regression to reduce the funnel shape effect of the residuals. This transformation compensated the increasing differences in standard deviation associated to higher figures, a common issue when simultaneously considering values with more than 1000-fold difference (Barbur et al. 1994) . In parallel, baculovirus infection and VLP assembly responses were converted using the logistic regression to limit the possible values of the functions to the 0-100% range:

where Y n is the converted response and y n is the experimental response in natural values. A Box-Behnken design was used to determine the influence of CCI, MOI, and TOH on each evaluated response. These variables were screened at a low (− 1), medium (0), and high level (+ 1) as indicated in Table 1 . The different levels were linearly related for CCI and TOH and exponentially for MOI, always in an equidistant manner. The results obtained for each response were fitted to a second-order polynomial by the least squares method (Eq. 3):

where Y is the response variable, β 0 is the model intercept term, β 1 − β 9 are the model coefficients, and ε is the experimental error. Fitting of the different equations based on Eq. 3 was performed with the R software (R Foundation for Statistical Computing, Vienna, Austria). Three-dimensional plots were constructed to facilitate model interpretation.

The most common DoE approach involves the optimization of a single response. However, such analysis may not be enough for the BEVS, since the definition of a production condition cannot be accurately predicted from an individual property. Then, the objective of including more than one response in the study was to determine global conditions integrating different key aspects of the BEVS. To this purpose, a multiple-criteria decision analysis (MCDA) based on desirability functions was implemented. The different responses were transformed to a dimensionless desirability scale (d n ) ranging between 0 and 1:

where y n is the predicted response of the fitted equation, d n is the desirability response function, w accounts for the weight value, and min n and max n are the minimum and maximum acceptable values of y n , respectively. The weight (w value) NS non-statistically significant depended on the relative importance assigned to each individual response. Then, all the different desirability response functions under study were combined into a single equation, denoted as overall desirability (OD):

where OD is the overall desirability function to be maximized and N is the number of responses studied in the optimization process.

The experimental design and statistical analyses of the different equations were performed using R software. The quality of the regression of the fitted equations was evaluated with the R 2 and adjusted R 2 coefficients in percentage units. An analysis of variance (ANOVA) F test was used to determine the significance of the equations and the individual coefficients were assessed with a t test. The lack-of-fit (LOF) test was used to evaluate differences between experimental and pure error of the fitted equations. In all analyses, p values of 0.05 and 0.1 were considered statistically significant with 95% and 90% confidence, respectively.

Initially, the growth of High Five cells was characterized to determine an adequate range of viable cell concentration at infection (CCI) for the DoE. Cells maintained a high viability (> 90%) until 96 h of culture, coinciding with the peak of viable cell concentration. In these conditions, cells reached a maximum of 7.3 ± 0.2 × 10 6 cells/mL and a doubling time (T d ) of 18.7 ± 0.5 h (Fig. 1) . Considering the extent of the exponential phase and the T d , the range for cell concentration at infection was restricted to 0.5-2.5 × 10 6 cells/mL. Some difficulties were encountered when defining the different levels of multiplicity of infection (MOI) and time of harvest (TOH) since very little information on the use of the BEVS with High Five cells in the Sf900III medium was available. The ranges for both variables were eventually fixed according to previous experience with this system (data not shown) and based on studies of the High Five/BEVS in other cell culture media (Sander and Harrysson 2007; Pillay et al. 2009 ). The MOI experimental range was fixed between 0.01 and 5 with the aim to screen low and high MOI conditions in the same DoE. In the case of TOH, the boundaries were defined as 24-84 hpi. DoE space boundaries did not involve high CCI out of the exponential phase or medium exchange in order to simplify their industrial application, but these conditions were evaluated as a contrast to the optimal conditions obtained as further presented.

Combining RSM and MCDA to define the optimal VLP production conditions A three-variable (CCI, MOI, and TOH) Box-Behnken RSM was constructed and the following objective responses were analyzed: baculovirus infection efficiency, VLP production, VLP assembly, and VLP productivity. This experimental design was selected among different candidates due to its variance distribution and spatial properties ( (Table 1) . The different datasets were adjusted to the second-order polynomial functions by the least squares method according to Eq. 3. The statistical significance of the different functions and their associated coefficients was confirmed by ANOVA (Table 1) . Each function was used to construct three-dimensional plots for a better comprehension of the synergies between CCI, MOI, and TOH (Fig. 2) . As expected, baculovirus infection progressed more rapidly with increasing MOI (Fig. 2a-c) . However, the pace of infection decreased when using the same MOI at higher CCI. A similar behavior was observed between VLP production and VLP productivity ( Fig. 2d-i) . Low MOI required longer TOH to achieve higher VLP yields, whereas higher MOI shortened this period. In both cases, the best production and productivity titers were obtained in the 1.5-2.5 × 10 6 cell/mL CCI range. TOH also proved to be the most significant variable regarding the amount of GageGFP monomer assembled in the form of VLPs (Fig. 2j-l) . Increasing TOH and MOI substantially decreased the ratio of VLPs to non-assembled monomers, regardless the value of CCI. The models were used to predict an optimal combination of CCI, MOI and TOH to maximize each specific response. In this case, different independent variable combinations resulted in the optimum condition for each function (Table 2 ), thus making difficult to define a global optimum condition combining all the different models at once. Therefore, a multiple- Fig. 2 Three-dimensional plots of the different functions based on the Box-Behnken experimental results. a-c Baculovirus infection. d-f VLP production. g-i VLP productivity. j-l VLP assembly as a function of CCI, MOI, and TOH. All the graphs were constructed by representing the effect of two independent variables on a response while maintaining the third one at a fixed level criteria decision analysis (MCDA) based on desirability functions was applied in order to determine a global optimum combining the different functions. Every model function was transformed to a dimensionless scale (Eq. 4) and given a weight according to the importance of each response. A higher priority was assigned to VLP production, VLP assembly, and VLP productivity (w = 2), while a lower restriction was assigned to infection (w = 1). Two possible response combinations were considered in the MCDA, the first focused on maximizing product quantity and the second one maximizing product quality. To do this, the VLP assembly function was excluded from the MCDA in the definition of a global optimal condition targeting product quantity. The application of the MCDA for the product quality optimum resulted in a CCI, MOI, and TOH of 1.1 × 10 6 cell/mL, 1 pfu/cell, and 33.6 hpi, respectively. The optimum maximizing product quantity was determined as 2.0 × 10 6 cell/mL for CCI, a MOI of 2.5 pfu/cell, and a TOH of 69.3 hpi.

The two global optimal conditions obtained by the combination of RSM and MCDA were successfully corroborated in a validation experiment. High Five cell growth was arrested after BV-GageGFP infection with > 80% of the culture infected at 24 hpi ( Fig. 3a-b) . As expected, a higher cell viability was observed for the quality optima (33.6 hpi) compared with the quantity condition at TOH (69.3 hpi). Confocal microscopy analysis of infected cells showed successful colocalization (yellow) of the GageGFP polyprotein (green) with the cell membrane (red), thus indicating that VLP formation and production was taking place (Fig. 3c) . This process could be tracked in real time using a confocal fluorescence microscope with the high-speed acquisition mode (Fig. S1) .

Measurement of fluorescence indicated that the highest pace of GageGFP production was achieved with higher MOI. Also, the highest fluorescence yield in the supernatant was achieved with the quantity optimum (2448.6 ± 23.8 RFU) at 69.3 hpi (Fig. 4a) . The TOH for the quality optimum condition coincided with the peak of intracellular GageGFP production, but not for the quantity optimum. In all cases, GageGFP production in the supernatant progressively increased with longer TOH, although the intracellular GageGFP levels reached a maximum concentration that subsequently decreased (Fig. 4b) . Analysis of the VLP production process of the quantity optimum by flow virometry evidenced that there was a continuous increase in VLP concentration (Fig. 4c) . Comparison of VLP production in both optima by means of nanoparticle tracking analysis (NTA) yielded a 10fold and 4.8-fold increase in production and productivity in the quantity over the quality optimum, respectively. In all cases, the experimental outcome was within the predicted limits (Table 3) . Similar ratios of VLPs to total nanoparticles were observed, representing a 9.7 ± 3.1% for the quality and a 9.3 ± 1.1% for the quantity condition. In contrast, analysis of the optima by sucrose cushion ultracentrifugation showed a 4.9-fold increase of GageGFP monomer assembled in the form of VLPs in the quality optimum (64.6 ± 5.1%). The SN and SN -25% fractions, corresponding to non-assembled GageGFP, showed significantly larger levels of fluorescence in the quantity optimum (Fig. 4d) . However, VLP-containing fractions (25-45% and 45%) were more enriched in the quality condition. BV-GageGFP titration of both optima by plaque assay resulted in a 2.7-fold increase of infectious particles in the quantity (13.2 ± 5.1 × 10 7 pfu/mL) compared with quality condition (4.8 ± 1.5 × 10 7 pfu/mL).

An acceptable correlation between indirect VLP quantification with spectrofluorometry and direct nanoparticle measurement with NTA was only achieved for the quality optimum condition (Eq. 1). On the contrary, GageGFP fluorescence levels of the quantity optimum measured by spectrofluorometry (2448.6 ± 23.8 RFU) and their conversion to VLP concentration according to Eq. 1 resulted in a 9.6-fold higher value than the one obtained by direct VLP quantification using NTA. However, multiplying this fluorescence value by the VLP assembly factor calculated by analytical ultracentrifugation (Table 3 ) allowed to determine the GageGFP fluorescence exclusively attributed to VLPs (323.2 ± 3.1 RFU) and discard that of unassembled GageGFP monomer. Introducing the fluorescence value associated to VLPs in Eq. 1 resulted in a better prediction to NTA quantification (4.9 ± 0.5 × 10 10 VLP/mL). Supernatant characterization of the quality and quantity optima by cryogenic transmission electron microscopy (cryo-TEM) indicated that VLPs were correctly formed in both conditions (Fig. 5) . Interestingly, the median VLP size was higher in the quality (181.4 ± 4.4 nm) compared with the quantity optimum (164.7 ± 0.3 nm). The presence of EVs and baculoviruses was also detected, in agreement with the existence of a non-fluorescent particle population observed with NTA.

In addition to the optimization work performed, the quantity optimum condition was compared with two conditions used in other works for the production of high VLP titers in order to corroborate the results of the study. The first approach consisted in infecting High Five cells at a high cell concentration and MOI. To this purpose, High Five cells were infected at 6 × 10 6 cell/mL with a MOI of 5. The second strategy consisted in performing a medium replacement before infection using the quantity optimum. This option was considered as a means to value if the added effort of performing a medium replacement would provide a substantial advantage in VLP concentration. Both conditions were not examined in the DoE in order to avoid the added difficulties required at process level, but were compared with the quantity optimum as a contrast since they have been used in the literature. Baculovirus infection progressed more rapidly after medium exchange than in the original condition but the drop in cell viability was not significantly affected ( Fig. 6a-b) . On the other hand, baculovirus infection advanced more slowly in the high CCI condition, to the point that cell culture was not fully infected after 72 hpi. Medium exchange before infection increased GageGFP production by 1.3-fold at 69.3 hpi, corresponding to 3168.6 ± 100.2 RFU in comparison with the 2528.0 ± 76.3 RFU achieved in the quantity condition ( Fig. 6c-d) . The same improvement was observed in VLP quantification by NTA, with 4.3 ± 0.2 × 10 10 VLP/mL for medium exchange while 3.4 ± 0.3 × 10 10 VLP/mL was measured for the quantity optimum condition. However, baculovirus infection at the high CCI condition reached a significantly lower GageGFP production (66.6 ± 3.3 RFU) and also in terms of VLP production (2.3 ± 0.6 × 10 8 VLP/mL). The median size of the VLPs produced in these conditions did not substantially vary from the quantity optimum (168.2 ± 3.3 nm), being 169.6 ± 3.3 nm for the medium exchange and 160.5 ± 3.7 nm for the high CCI. Similar levels of total nanoparticles were obtained in the three different conditions, thus representing a big difference in the ratio of VLP to total nanoparticles (Table 4 ). Remarkable differences were also observed as regards the amount of infectious baculovirus particles produced. Medium replacement before infection increased the levels by 2.1-fold (47.0 ± 9.9 × 10 7 pfu/mL) compared with tested. Infected cells were measured every 24 h until their optimal TOH. c High Five cells infected with the BV-GageGFP at 2.0 × 10 6 cell/mL and a MOI of 2.5 and observed at 48 hpi. Cell nucleus was stained with Hoechst (blue) and cell membrane with CellMask™ (red). The mean and standard deviation of triplicate experiments are represented the 22.7 ± 2.5 × 10 7 pfu/mL achieved in the quantity optimum condition. However, a much lower baculovirus titer of 0.9 ± 0.3 × 10 7 pfu/mL was obtained in the high CCI condition.

The High Five/BEVS has demonstrated a high versatility to produce a wide variety of recombinant proteins. However, the capabilities of the High Five cell line as a production platform of complex multimeric structures, such as enveloped VLPs, have not been explored in detail. To date, the assessment of VLP production has been performed based on indirect quantification methods (Pillay et al. 2009 ). Moreover, most of the research has been conducted either in low performing or animal compound containing cell culture media (Krammer et al. 2010; Wilde et al. 2014) . Although these works have brought advances in the production of nanoparticles using the High Five/BEVS, a deeper study would contribute to exploit the full potential of such platform. CCI, MOI, and TOH were selected as the critical parameters affecting the production of HIV-1 Gag VLPs in the BEVS. For a comprehensive analysis, four different responses were considered and simultaneously evaluated by means of RSM and MCDA. TOH and MOI were shown to be particularly relevant to achieve a high VLP concentration but also in Fig. 6 Comparison of VLP production using the quantity optimum with medium exchange and baculovirus infection at a high CCI. a-b Viable cell concentration, cell viability, and BV-GageGFP infection process in the different conditions tested. c-d Supernatant and intracellular GageGFP production. The average of triplicate experiments is represented. Medium exchange was performed prior to BV-GageGFP infection and consisted in infecting High Five cells at 2.0 × 10 6 cell/mL with a MOI of 2.5 pfu/cell. As regards the high CCI condition, High Five cells were infected at 6 × 10 6 cell/mL with a MOI of 5 maintaining an adequate ratio of GageGFP assembly in the form of VLPs. Pillay and co-workers used a factorial experiment to assess the effect of different MOI comprised in the range of 0.1-5 in High Five cells (Pillay et al. 2009 ). They did not identify any significant difference in Gag yield, but here we observed that MOI plays a significant role in VLP production. Interestingly, including a function for VLP assembly based on the measurement of the GageGFP fluorescence distribution in the different fractions of an ultracentrifugation proved to be highly relevant. These results in combination with direct nanoparticle quantification by NTA and flow virometry permitted to obtain a more accurate perspective of the process.

A pronounced decrease in VLP assembly was shown with increasing TOH, limiting a favorable combination with the other three responses. To this purpose, two different global optimization strategies were examined by MCDA, one considering the VLP assembly function (therefore with priority on product quality) and the other not (therefore with priority on product quantity). Remarkable differences were encountered between the two optima, achieving a 10-fold higher VLP production in the quantity condition, whereas a 4.9-fold increase in the assembly of GageGFP as VLPs was obtained in the quality optimum. Then, it is evident that High Five cells possess a high capacity to produce GageGFP, but there is a remarkable competition between the formation of VLPs and the release of unassembled GageGFP monomer. The large amount of GageGFP produced, potentially overcoming the capacity of the cell line itself to process all the GageGFP in the form of VLPs, combined to cell membrane disruption could be the reason explaining these results. This could be appreciated even in the quality optimum itself, in which a high cell viability of 92.4 ± 0.6% was measured at harvest (33.6 hpi) (Fig. 3a) and a 64.6 ± 5.1% of the fluorescence in the supernatant was associated to VLPs, meaning that around the 35% remaining was due to unassembled GageGFP monomer. These results emphasize the need to complement the methods most currently used for VLP identification or quantification based on monomer detection with direct nanoparticle assessment techniques, specially using the High Five cell line (Maranga et al. 2003; Pillay et al. 2009; Tagliamonte et al. 2010; Shoja et al. 2013; Monteiro et al. 2016; Fuenmayor et al. 2019 ).

The application of cryo-TEM helped to gain insight into the identification of the morphological features of the VLPs produced (Fig. 5) . Cryo-TEM has recently been highlighted as powerful methodology for nanoparticle characterization as the different specimens can be observed in native conditions (Martin et al. 2016; Maldonado et al. 2016; Gallagher et al. 2018) . GageGFP VLPs presented the expected size of 100-200 nm and morphology consistent with immature HIV-1 VLPs, comparable with VLPs produced in Sf9 (Nika et al. 2017 ) and HEK 293 cells (Venereo-Sanchez et al. 2016 ). The rod-shaped structure corresponding to the infective form of the baculovirus was also detected. The presence of EVs was observed alongside VLPs, which are known to be produced as way of communication in eukaryotic cells (Ratajczak et al. 2006) . EVs were more heterogeneous in size (50-500 nm) and shape compared with VLPs and less electron-dense. These results coincide with the measurements performed by NTA and flow virometry where a remarkable population of non-fluorescent nanoparticles was detected. Future efforts are needed to understand their role in insect cell lines since little information is available.

A maximum HIV-1 GageGFP VLP concentration of 3.9 ± 0.1 × 10 10 VLP/mL was achieved in the supernatant using the product quantity optimum. Thus, these conditions would be selected in case of designing a VLP manufacturing process. However, if the presence of baculoviruses posed a risk for the final VLP application, the quality optimum provides a 2.7-fold reduction in infectious particles, which would facilitate the downstream process. Difficulties were encountered in the comparison of the VLP titer obtained since most of the studies producing Gag VLPs with the insect cell/BEVS used indirect quantification methods based on monomer detection (Buonaguro et al. 2001; Pillay et al. 2009; Visciano et al. 2011) . Nevertheless, when the comparison of nanoparticle production was possible, this optimum condition proved to be superior to Gag VLP production in HEK 293 cells without ) and with additive supplementation (Cervera et al. 2015a ) by 14.4 and 1.7-fold, respectively. Moreover, these conditions proved to be superior to influenza VLP production using the Sf9 (Thompson et al. 2015) and High Five/BEVS (Carvalho et al. 2016 ) by 6.7 and 25-fold, respectively. The potential of the quantity optimum was also evaluated against other baculovirus infection strategies in this work. Infection at a high CCI using a high MOI resulted in a much lower yield of VLP production probably owing to the scarcity of some nutrients in the medium (Table 4 ). BV production was also significantly reduced in such conditions. These differences in production could be related to the cell density effect previously described in insect cells with the BEVS Huynh et al. 2013; Huynh et al. 2014 ). On the other side, medium replacement before BV infection moderately increased VLP production but duplicated baculovirus production. This strategy has proven to be an efficient manner to increase both the yield of recombinant proteins (Caron et al. 1990 ) and baculoviruses ) with the Sf9/ BEVS cells and also in mammalian cells (Bollin et al. 2011; Cervera et al. 2015b) . In this case, no substantial benefit was obtained, thus indicating that the added efforts required to perform medium replacement might not be advantageous.

In conclusion, a detailed study of Gag VLP production using the High Five/BEVS was conducted. The application of RSM and MCDA allowed to go a step further and capture the synergies between the influential factors affecting the VLP production process. The combination of advanced statistical methods with a variety of nanoparticle quantification and characterization techniques allowed to obtain a more comprehensive picture of the process and to determine a highyielding and reproducible condition for VLP production. The approach here proposed is valuable for studies dealing with the production of other complex nanoparticles. Future efforts in transferring this process into bioreactor scale should allow to define a robust platform for VLP production.

Virus-like-vaccines against HIV

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Generation of HIV-1 Gag VLPs by transient transfection of HEK 293 suspension cell cultures using an optimized animal-derived component free medium

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Nanoscale characterization coupled to multi-parametric optimization of Hi5 cell transient gene expression

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Conflict of interest The authors declare that they have no competing interests.Ethical approval This article does not contain any studies with human participants performed by any of the authors.

